Process for forming catalytic amorphous glass fibers

ABSTRACT

Catalytic, amorphous glass in highly divided form, such as fibers, is disclosed in which the glass is substantially noncrystalline and contains from about 10 percent to about 70 percent by weight of an essentially binary system comprising at least 5 percent by weight of the glass of CuO and the balance of a metal oxide selected from the group consisting of MnO2, Cr2O3, Fe2O3, CoO, NiO, V2O5, La2O3, CeO2, ZrO2, and mixtures thereof. Where used, the fibers are prepared by fiberizing such a glass composition and then cooling the resulting glass fibers at a sufficiently fast rate to obtain little or no crystallinity. Optionally, the amorphous glass composition may be used as a powder.

United States Patent 1191 Roberts Sept. 23, 1975 PROCESS FOR FORMING CATALYTIC AMORPHOUS GLASS FIBERS [75] lnventor: Gordon J. Roberts, Shaker Heights,

21 Appl. No.: 532,307

Related US. Application Data [62] Division of Ser. No. 279.211, Aug. 9. 1972, Pat. No.

[52] US. Cl. 65/2; 106/50; 106/48; 252/476; 252/462; 252/432; 252/455 R;

. 252/471; 252/467; 252/474 [51'] Int. Cl. ...C03C 13/00; 1301.] 11/32; B01J 11/22 3547,0911 12/1970 106/48 3.562.184 2/1971 106/48 3.671.278 o/19'72 Borowski 106/48 3,718,498 2/1973 Denny et .11. 106/48 3.748,]71 7/1973 Pedeling 106/48 Primary E.\am1']1erPatrick P. Garvin Assistant Exam'ifiev-Mark Bell Attorney, Agent, or FirmMilton L. Simmons; Wesley B. Taylor [57] ABSTRACT Catalytic, amorphous glass in highly divided form, such as fibers, is disclosed in which the glass is substantially non-crystalline and contains from about 10 percent to about 70 percent by weight of an essentially binary system comprising at least 5 percent by weight of the glass of CuO and the balance of a metal oxide selected from the group consisting of MnO- Cr- O Fe O CoO, NiO, V 0 La O CeO ZrO and mixtures thereof. Where used, the fibers are prepared by fiberizing such a glass composition and then cooling the resulting glass fibers at a sufficiently fast rate to obtain little or no crystallinity. Optionally, the amorphous glass composition may be used as a pow der.

4 Claims, 2 Drawing Figures US Patent Sept. 23,1975 Sheet 1 of2 3,907,532

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US Patent Sept. 23,1975 Sheet 2 of2 3,907,532

z o m u m 2 mmmsbcz MQXO Q5555 2353 .0 mzoEmoniou kzmowma 50m;

CROSS-REFERENCE To RELATED APPLICATION This application is a division of'application Ser. Nol 5 BAcKoRou o or THE INVENTLON A- porcelain enamel frit' containing an oxidation- 16 inducing metal oxidc, such as cobalt oxide, has been suggested forexample, in U.S.Pat. No. 3,547,098 to Lee. Such frit may be used asa porcelain enamel coating for-oven liners,'or the like, where its ability when heated to oxidize foreign matter such as oven soils con-,

verts theovcn to a desired self-clcaningwtype. Still other applications for the fritare possible, such as informing vitreous coatings for exhaust systems, of;paint-baking ovens or au tom'otive exhaust systems, the;interiors of which can becoated with-enamel from the frit to ren- 20 der passing gases less noxious and objectionable prior to their discharge from, the systems by oxidizing the gases- I 1 1 y lthough the present invention ,is not to be bound by theory, it isgenerallyaccepted that for a certain mate- 2'5 rial to have a catalyticeffect, such asin oxidationinducing, the material must have active sites of po tentially high chemical activity. To one skilled in the art, this means a crystalline structurein which atoms of materials are arranged in preordained fashion, According conventional oxide catalysts are microcrystalline solids. As ajrule of thumb, the smaller the crystalline size of such oxide catalysts, the more active it is. If a catalyst is exposed to excessive "heat during its useful ity decreases. 1 v s s The use of glass fibers whicharewell known to be amorphous'and non-crystalline would not, therefore, by expected to 'be useful for catalytic, oxidationinducing activity Nor would amor phous'glass in other forms. such as powder, be expected to be catalytically active. In a copendin g'application, filed in the names of Walter H. Brueggemann and Jack S. Gilhart on Aug. 9, 1972, entitled Catalytic Crystalline Glass Fibers," Se'r. No; 279,210, now Us. Patina. 3,873,328, and as signed to the assignee'of this application, amorphous glass fibers containing an oxidation-inducing oxide are made catalytic by heat treating the glass f bers to convert them into a crystalline form. In accordance with the present inventionyamorphous glass in "highly'divided form, such as glass fibers, is provided which is alwaysamorphous, n'eed' not be crystallized, and yet is capable of catalytic, oxidation inducing activity.

SUMMARY oF THE INVENTION life, the crystallite size increases and the catalytic 'activ- 40 i The present 1nven-t1on resides In using a base glass composition of substantially inert, glass-forming m'at'e' rials containing from about IO'percent to about'7O peri cent by weight of an essentiallybinary metal oxide system converting the molten compositionto a highly 5 divided such as by fiberi zing and cooling th'efibers ja'gs' ufficienfly fast rate to avoid substantial crys talliza'tion. The resulting glass fibers are used in't'he 2 amorphous form and are found to have good catalytic. oxidation inducing effect on combustible materials. Alternativcly the glass composition may be used as a powder. i g i The essentially binary metal oxide system comprises at'lcast 5 percent by weight ofthe glass composition of CuO and the'balance of the 10 percent to percent fraction ofa'metal oxide selected from the group consisting of MnO Cr O Fe O CoO. NiO 1211,05,, CeO- ZrO and mixtures thereof. In the' preferred practice. a substantially ternary system is employed. such as in weight percent from about ZS' p e rcent to about percent of CuO, from about 25 percent to about 62 percent of MnO and up to 50 percent of an adjuvant oxide which may be any one or more of the remaining oxides listed. preferably Cr O or R 0 The metal oxides are mixed with the base glass composition and fiberized by known conventional means as long as the fibers are rapidly chilled to avoid substantial crystallization. A powder'may be formed by grinding the fibers. I l

The glass fibers may be used in any conventional manner, such as in batt, met. or glass wool form, and

mounted in a given installation as to be exposed to material of which at least partial oxidation is'to made. Thehigli surface area of the glass fibers considerably improves intimate contact between such material and the catalytic fibers to promote combustion or other" chemical changes. The fibers effectively supply oxygen when combustible materials contact them, while oxy gen from the atmosphere is absorbed by fibers and, it is theorized, stored or diffused throughout the body of the glass fiber. In this manner sufficient excess oxygen is available to promote oxidation as desired when the fibers are subsequently heated to an oxidizing tcmpe raturc. This oxidation absorption phenomenon seems to occur at about the same temperature as needed for oxidation of combustible material contactingthe glass fiber surface. The powder form of the present glass compositions may be used as such or placed on a conventional carrier such as of alumina. I

It is theorized that when a present glass composition is, for example, fiberized and rapidly chilled. the resultant solid vitreous or amorphous material still possesses a disorganized, liquid-like molecular structure. It is postulated that the theoretically desirable coordination requirements of the metal ions on the surface of the glass fibers have not been satisfied. This may leave defects similar to crystalline structural defects which define adsorptive sites'capable of catalytieactivity. The increased surface area afforded by a powder or fiber is also thought'to becontributory.

R E DESCRIPTION O THE N'G -In the accompanyingdrawingz- FIG. 1 is a three-component composition'diagram of one desirable metal oxide ternary system for use in the present glass composition; and

FIG. 2 is a three-component composition diagram of another desirable metal oxide ternary system for use in the present invention. In both figures, the numbers refer to the corresponding example numbers in Tables I and IV.

DESCRIPTION'OF THE PREFERRED EMBODIMENTS composition used in. conjunction with an oxidationinducirigmetaloxide system as more fully described hereinafter As such. the base glass merelyse rvcs as a vehicle in which to dissolve and transport a binary oxide system and therefore may comprise anygcncrally known glass-forming matcrials. usu al ly other oxides. When fibers are to .be prepared, the base .glass should have a fusibility and other physical characteristics as to be fiber ized by standard known means. However, changes and adjustments in the base glass maybe made in order better to adapt the glass fibers for their in;

4. A lk all-frce magnesium alurriinosilicate glasses.

The binary metal oxide system is characterized herein as essentially" binary, since it must comprise, copper oxide and a second adjuvant metal oxide which may be one of several oxides or mixtures thereof.v For example ,.'the.adjuvant oxide may beYMnO Cr O Fe Q CoO, NiO, V 05, La O CeO ZrO or mixtu res of two or more of such oxides. The metal oxide system is added to thebase glass composition so as to comprise from about to about 70% by weight of the total. 1 s I i l There are preferred binary and ternary oxide systems. Forexample a preferred binary system itself comprises in weight percent about:

Percent I CuO to 80 MnO-; .20 to 75 Ternary preferably .include'the following in' weight percent:

Percent ctto 25 to so MnO 20 to 75 A I Adjuvant Oxide 0 10755;

The adjuvant oxide may be any one ormore of the remaining metal oxides previously mentioned. The preferred "adjuvant oxides are chromic oxide'and ferrie'oxide. The preferred weight percent composition of-systems containing .these oxides are-as third oxide are:

Percent W Clio" ssmso "MnO lOlo55""-" CHO l0t032j,5 t "Percent;

CuO to. 70: MnO-, 8 to 42 lie O l9 to 60.

Highly desirable tergnarymetal oxide systems include in weight percent 63 percent CuO. I] percent Cr- O and Z Opercent MnOi and 46 percent 'CuO. 9 percent MnO and ,45 percent Fe O .ln the foregoing systems expressed in percentage, i'tis understood that sufficient amounts of the indicated oxides are present to total] 00 percent. 4

The total glass compositions,that"is, base glass plus metalzoxide system. may be; prepared in any desired manner, as by.-admixing the components whilexin a dry state. The particle sizes of the oxides are not critical, since the entire mass is eventually melted-The melting is followed by-fiberization which may be carried out by conventional, known equipmentasu'c-h as'byenveloping a fine molten stream'of the glassm a blast of air and attenua'ting. the stream into-fine, usually discontinuous fibers which are collected-on a screen in interlaced mat or battform. ltisnot necessary to use a binder for the fibers, btifi'f one isapplied iti mus t be resistant to the temperatures 'atwhich the'mat'or batt willbe used in practice. The size of the fibers is'dictat'ed more by their particular eventual application, rather than the fiberizirig techniqueemployedI'Glass-fibers of standard-dimensions are satisfactory; ln general, the fibers can be of any reasonable length and preferably have at least a sufficiently small diametertorender the'fibe'rs flexible. As glass compositions of the present'invention are' fl berized; the fibers must becooled 'o'rchille'd sufficiently fast to avoid crystallization and to preserve the desired (for the"pr esent' composition) amorphous state.' it is possible to tolerate some crystallization without losing the advantages of the present inventioni Indeed, it jmay be virtually impossible or, impracticalto avoid incipient crystallization.Crystallization up to'at least 10 percent of the mass can be tolerated without serious loss of catalytic :act'ivity. Normally, crystallization is less than '5 percent of the rnas s. 3 I V 7 After the glass composition is fiberized and the fibers chilled and collected in -a desiredphysical form, they be installed'a's desired in any environmentin which at least partial oxidation of a combustible material is desired, For example, a bodyjoftibers may be installed 'along one or more walls of an oven to oxidize oven soils. Or a'mat of the present glass fibers may line an automotive muffler or other chamber ,in anautomotive exhaust system to oxidize. gases, such as ,carbon monQxide to carbon dioxide Generally, little or no effective- .oxidation can be achieved belowa temperature of,

' about 3,50F., while the upper temperature limit of oxi-.

dation utilizing the presentglass fibers is inthe vicinity ofabout 7Q0F..

'letizing mixturesef the present pulverulent amorphous glass compositions vand particles of alumina,; silica, magnesia, titania, zirconia, calcium sulfate, or the like;

MnO

The following examples are intended to illustrate the invention and should not be construed as imposing lim- 6 Three gas mixtures used were composed as follows: a. 1 percent CO, 3.75 percent air. remainder nitrtr itations on the claims. gen; 1 I 1 V b. lpercent ethylene. 22.5 percent air. remainder ni- EXAMPLES 1 through 14 5 tmgefi; and g I V Table 1 lists 14 different batch weight (parts by c. 0.25 percent ethylene. 5.6 percent air. remainder weight) glass compositions ofthe present invention emnitrogen. i bodying a base glass as designated by the first five listed In each case the amount of air present was 50 percent ingredients. a binary system of CuO MnO and a terin excess of that needed for complete combustion of ,riarymetal oxide system of MnO -CuO-Cr O The base the combustible component. Samples of the inlet and glass was the same in each case to provide a basis of exhaust gases were withdrawn from the apparatus pericomparison, the relative amounts of the oxide systems odically by means of a valve system and subjected to being varied. The base glass comprised 50 mole peranalysis by gas chromatography. The reduction in -cent of the finished composition, the oxides account, amount of the combustible component in the exhaust TABLE I Glass Batch Compositions Based on the CuO-MnO and MnO CuO-CQQ Catalyst Systems (Parts By Weight) Example 1 2 3 4 5 6 7 8 v 9 10 11 12 i 13 14 Borax 14.4 i 14.4 14.4 14.4 14.4 14.4 14.4 14.4 14.4 14.4 14.4 '14.4 14.4 14.4 Soda Ash 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0 18.0

Potassium Carbonate 31.25 31.25 31.25 31.25 31.25 31.25 31.25 31 31.25 31.25 31.25 31.25 31.25 31.25 Silica 84.0 84:0 8410 i 84.0 84.0 84.0 84.0 84.0 84.0 84.0 84.0 84.0 84.0 84.0 Titania 39.6 39.6 39.6 39.6 39.6 39.6 39.6 39.6 39.6 39.6 39.6 39.6 39.6 39.6 .Cr O 19.0 19.0 19.0 19.0 19.0 38.0 38.0 9.5 28.5 9.5 28.5 9.5 28.5

CuO 40.0 50.0 60.0 70.0 80.0 70.0 60.0 55.0 50.0 65.0 60.0 75.0 70.0 700 54.25 43.0 32.5 10.9 11.0 22.0 43.0 37.6 32.5 27.1 21.75 16.3 32.5

ing for the other 50 mole percent. After melting, the base glass of the rrielt contained in mole percent: 4.8 percent of NaZO; 4.5 percent of K20, 2.8 percent B 0 28.0 percent of SiO2, and 9.9 percent of TiO After a particular glass composition was melted, the melt was fiberized by directing a molten glass stream of the melt axially through a metal venturi supplied with compressed air through an annular slit in the throat section of the venturi. The air was exhausted into a wooden box collector having screens l/l6-inch mesh on whichto collect the fibers. The air pressure used was in the range of about 100 to 150 p.s.i.

To test amorphous fibers of the present invention, a conventional vitreous, silica tubular reactor was used with provision for sampling a gas mixture both before and after passage through a catalystbed comprising the fibers under test stationed within the reactor. The internal diameter of the reactor tube was 0.75 inch. A chromel-alumel thermocouple was placed axially into the tubularieactor to apoint centrally of the proposed glass fiber bed and used .both as a catalyst support and as the temperature sensor. The amorphous catalytic fibers were then introduced and gently tapped down and I around "the thermocouple end until a bed was' formed i in place and to act as a gas preheater. The packed tube was then mounted in a suitable furnace whose temperature could be controlled as desired.

A gas mixture was then passed into the tubular reacwas used to calculate the percentage of that component oxidized by a single pass through the catalytic fibrous bed. I

Table 11 lists the percentage results an oxidizing carbon monoxide by amorphous glass fibers prepared from the compositions of Examples 1 through 4 of Table 1. Table 111 lists the percentage results of oxidizing ethylene (1 percent ethylene mixture) by many of the same examples of Table l as indicated. FIG. 1 illustrates a ternary composition area, delineated by the .examples of Table 1 having ternary metal oxide systems, which was found to have good catalytic activity even though the glass was in the form of amorphous glass fibers.

Glass composition of Example 4 was found to have an excellent catalytic activity.

EXAMPLES 15 through 26 Table IV lists 12, different batch weight (parts by weight) glass compositions of the presentinvention embodying a base glass and a ternary metal oxide system of MnO -CuO-Fe O Glass, fibers were prepared and tested from these glass compositions in the same manner as described for Examples 1 through 14. Table V (1 percent ethylene mixture) lists the percentage results of oxidizing ethylene by many of the examples of Table IV. FIG.

tor and through the catalyst bed. A fine needle valve in a gas mixture entrance line and a rotameter were used to adjust the flow of the gas mixture to a desired rate measured in liters per minute. i

2 illustrates a ternary composition area delineated by Examples 16 through 23 which was found to have good catalytic activity, even though as part of amorphous glass fibers. Glass compositions of Examples 17 and 18 were found to have excellent catalytic activity.

1 TABLE V Percentage Ohidiliipll ol Ethylene by Alkitlifrcc Catalytic Amorphous Glass FihersBasctl on MnO. .-CuO-Fe. Catalystsystcm 'lcmp- Flo\\' erature Rate Example (Cl (1.m 1 I5 16' 17 18 19 20 21 22 23 24 25 26 l /2 5618 66.9 74.7 54.4 55.1 48.0 61.0 43.1 95.3 84.2 82.1 325; 1 32.0 46.8 40.6 32.2 35.2 ).3 40.3 26.0 79.2 59.7 56.5 1 2 15.7 24.4 24.2 14.2 25.0 58.4 37.9 34.4 V 3 19.1 16.7 11.3 41.9 27.5 26.5 I .2 83.9 91.9 91.2 78.5 78.6 74.0 85.3 59.6 8 97.6 98.0 350 .1 56.8. 70.0 70.2 51.9 52.7 47.1 60.6 39.3 96.7 86.0 80.0 2 28.0" 38.7 37.6 30.3 36.3 28.8 37.6 28.3 81.5 60.2 55.4 1 3 22.0 31.6 24.6 17.4 26.3 31.8 27.1 61.8 43.5 49 4 =2 -97 I 91.3 91.8 93.0 76.0 375 1 79.3 90.8 90.4 72.3 70.0 74.0 84.0 55.6 94.8 r 2 '40.9 60.6 64.9 39.4 43.1 46.4 54.3 39.8 92.9 77.3 3 28.5 45.4 38.8 27.9 39.4 31.8 36.2 34.5 75.7 60.1 85.2 400 -97 91.0 82.6 90.3 6. .2 4 2 69.9 82. .81..4 54.9 57.0 57.2 71.9 48.5 91.2 V P 3 40.4 56.9 51.6 36.2 45.8 41.2 53.4 37.4 91.3 75.

3 NOTE implc 15 was tested with a 1'; C'. .H, gas mixture. giving rise to temperature stability problems in the catalyst bed; the reported results an: In. All subsequent Examples were tested with it'll-1'; (2H mixture.

EXAMPLES 27 through 31 These examples illustrate the use of quaternary metal oxide systems. Table VI lists five different smelted glass compositions of the present invention embodying a base glass and a quaternary metal oxide system of zirconia, copperoxide. maganese dioxide, and an additional oxide selected from one of five. namely CD103. Fe O V 0 C00 and N10. The base glass is the same in each instanceas represented by the first seven ingremerits.

, Glass fibers were prepared and tested from the glass compositions of Table V1 in the same manner as previous1y. descr ibed. Tablctvlllists the percentage results of oxidizing ethylene bythecompositions of Examples 27 through 31.

v EXAMPLE 32 'The following is a further example of a binaryoxide in a baseglass composition:

. :Batch Melt (Parts by Weight) (Weight '7;

86.4 27.0' Magnesia 14.4 4.5 Alumina 66.0 13.5 hydrate 1 (as A1 03) Titania 46.0 14.4

CoppcrOxidc 70.0 V 21.9 V 60.0 18.7

Ferric oxide The binary system comprised 53.9 weight percent of CuO and 46.1 weight percent of Fe O Fibers prepared from the melt were tested under conditions previously described and had the following percentage oxidation of ethylene at the indicated temperatures when the ethylene-air mixture was passed through a fibrous catalytic bed at a rate of 1 liter per minute.

Table VI Smelted Glass Compositions Based On Metal Oxide Quaternary Systems Percentage Oxidation of Ethylene 'by Catalytic Amorphous .Gluss Fibers Having Compositions from Table a;

I -5 "results; The term S.V. means space velocity" and: Tcmp- Flow I the value given indicates the number of volumes of gas eraturc Rate Exampe v (Dc) um) 27 2x 29 30 3| under test (standard conditlons) equal to the volume of catalyst that flows through the catalyst per hour. 25 i: 10 It is not clearly understood why the present amor- 2 I l phous glasses possess such catalytic 'activity as com- 3 T, pared to a crystalline catalyst. If. as is generally ac- 350 f Mg I 3 cepte d, one considers the presence of lattice defects in 2 4.6 6.7 0.9 21.8 a crystallmecatalyst to be largely responsible for its 3 3.2 5.3 5.4 6.3 1 lb M 294 4L7 M7 545 I5 catalyuc act1v1ty (as by offermg strong adsorptlon s1tes 375 1 14.4 16.7 25.4 41,0 'or by reducmg nearby bond strengths). 1t 1s postulated I '3; thatwhile amorphous materials can hardly be said to 1 115 458 555 613 1 have lattice defects, yet there must be surface imper- 400 g fections which act like a lattice defect of a crystalline 3 Q5 I 1 I 1 v0 catalyst. If a glass melt is quenched almost instanta- 42 1 a 13-: 22-2 'neously below its transformation temperature, as when 2 2;; 1: fibers are blown, it is possible that a large concentrai 16: 63.; 5.8 16.2 -tion of defects are frozen intothe glass structure. 450 l M 5 82.7 That there are such changes in the glass is evidenced by 2 20.1 14.2 27.8 38.7 changes 1n 1ts physleal propertles as compared w1th the l 3-: L f same glass composition when properly annealed, such 475 665 59.4 as, lower density, higher thermal expansion, poorer durablity, and the like. While the invention is not to be bound by theory, it seem possible that inthe light of the TABLE 1X Percentage Oxidation of Ethylene by Fibers of Compositions of Table Vlll' i I 1 l- Example m 11m (SW1 3230 hr. I) (S.Y. 6460"hr.")

300C -.;325c c 375C 375c 400C 4g5 cv i 33 22.4 f43.0 (15.1 .632 111:0 85.7 34 37.6 65.14 1 16.5 93.0 35 36.9 59.8 4 77.7 92.4? 1 V, 30 13.6 22.0 45.4 710 142.4 91.4, 37 15.9 1 41.7 611.7 73.5 s33 1444.7

.present invention a chilledvitreous fiber migh.t., have Percent more surface defects per unitof area thanacrystal 2252C ll. which had been heated to a moderate temperature as 3205 in; is the case with normal catalysts. I 2 400C 70.1 It is also significant that two or more metal oxides are EXAMPLES 33 through 37 Table Vlll lists batch recipes (parts by weight) for preparing present glass compositions having still other multi-oxide catalytic systems in an amorphous matrix.

Table v111 Glass Batch Compositions (Parts by Weight) YT he compositionswere smelted at about l475C.

Thecatalytic oxidation of fibers blown from these com- I positions wastested on ethylene-airmixtures using the technique previously described. Table IX contains the used in the present invention as represented by the described binary and ternary s'ys'ternsf The use of a plural- ,ity of metal oxides probably increases the range of interionic distances and bond energies. It is thought that such a surface havinga plurality of oxides may 'offer suitable adsorption sitesfora wide variety of gaseous molecules and therefore have a wider spectrum re sponse and be more capable of oxidizing a scope of dif-' ferent organic compounds.

While the foregoing describes several embodimens of the present invention, it is understood that the inven- .tion may be practiced in still other forms within'the scope of the following claims:

1 claim: l. A process for forming catalytic, amorphous glass fibers' leffective at temperatures within the range of about 350 1 to ()"F. two grams of said fibers. having 13 -a:-fiberizing a molten glass composition comprising .f'rom about lO-percent to about 70 percentby weightof an essentially binary metal oxide'system i and a balance of substantially,inertglass-forming amorphous materials, said oxide system comprising at least 5 percent by weight of said glass composition of C110 and the balance of a metal oxide seleeted from the group consisting of MnO (R Fe- 0 COO. NiO, V 0 La O CeO- ZrO and A mixtures thereof, and v Bl cooling the resulting fibers at a sufficiently fast rate to obtain less than crystallinity therein. 2 The process of claim 1 in which said metal oxide system is present as a mixture of oxides comprising in eight percent about:

i Pereent Cu() in so Mno 20 m 75 Adjuvant oxide 0 to 55 14 said adjuvant oxidebeing selected from the group consisting of Cr O F0 0;, (00. MO. V 0 Lil- 0 COO- ZrO and mixtures thereof. v

3. Theproeess of claim 1 in which said metal oxide system is present as a mixture of oxides comprising in weight percent about:

Percent CuO 35 to 80 MnO, I0 to 55 (IQ-() 10 to 31.

Percent C uO 30 to MnO, 8 to 42 F0 0 19 to 60 

1. A PROCESS FOR FORMING CATALYTIC, AMORPHOUS GLASS FIBERS EFFECTIVE AT TEMPERATURES WITHIN THE RANGE OF ABOUT 350*F TO 700*F, TWO GRAMS OF SAID FIBERS HAVING SUFFICIENT OXIDATIVE CATALYRIC ACTIVITY TO OXIDIZE ALL OF THE CO TO CO2 IN A SUPPLY GAS CONSISTING ESSENTIALLY OF 1 PERCENT CO, 3,75 PERCENT AIR BALANCE NITROGEN, AT A FLOW RATE OF ONE PER MINUTE AT 350*F COMPRISING: A. FIBERIZING A MOLTEN GLASS COMPOSITION COMPRISING FROM ABOUT 10 PERCENT TO ABOUT 70 PERCENT BY WEIGHT OF AN ESSENTIALLY BINARY METAL OXIDE SYSTEM AND A BALANCE OF SUBSTANTIALLY INERT GLASS-FORMING AMORPHOUS MATERIALS, SAID OXIDE SYSTEM COMPRISING AT LEAST 5 PERCENT BY WEIGHT OF SAID GLASS COMPOSITION OF CUO AND THE BALANCE OF A METAL OXIDE SELECTED FROM THE GROUP CONSISTING OF MNO2, CR22O3, FE22O3, COO, NIO, V2O5, LA2O3, CEO2, ZRO2, AND MIXTURES THEREOF, AND B. COOLING TE RESULTING FIBERS AT A SUFFICIENTLY FAST RATE TO OBTAIN LESS THAN 10% CYSTALLINITY THEREIN.
 2. The process of claim 1 in which said metal oxide system is present as a mixture of oxides comprising in weight percent about:
 3. The process of claim 1 in which said metal oxide system is present as a mixture of oxides comprising in weight percent about:
 4. The process of claim 1 in which said metal oxide system is present as a mixture of oxides comprising in weight percent about: 